SK133696A3 - Split flow reactor trays for vertical staged polycondensation reactors - Google Patents

Split flow reactor trays for vertical staged polycondensation reactors Download PDF

Info

Publication number
SK133696A3
SK133696A3 SK1336-96A SK133696A SK133696A3 SK 133696 A3 SK133696 A3 SK 133696A3 SK 133696 A SK133696 A SK 133696A SK 133696 A3 SK133696 A3 SK 133696A3
Authority
SK
Slovakia
Prior art keywords
tray
reactor
liquid polymer
flow
liquid
Prior art date
Application number
SK1336-96A
Other languages
English (en)
Slovak (sk)
Inventor
Thomas L Yount
Larry C Windes
James W Adams
Original Assignee
Eastman Chem Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Eastman Chem Co filed Critical Eastman Chem Co
Publication of SK133696A3 publication Critical patent/SK133696A3/sk

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14—Fractional distillation or use of a fractionation or rectification column
    • B01D3/16—Fractionating columns in which vapour bubbles through liquid
    • B01D3/166—Heating and/or cooling of plates
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14—Fractional distillation or use of a fractionation or rectification column
    • B01D3/16—Fractionating columns in which vapour bubbles through liquid
    • B01D3/18—Fractionating columns in which vapour bubbles through liquid with horizontal bubble plates
    • B01D3/20—Bubble caps; Risers for vapour; Discharge pipes for liquid
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14—Fractional distillation or use of a fractionation or rectification column
    • B01D3/16—Fractionating columns in which vapour bubbles through liquid
    • B01D3/24—Fractionating columns in which vapour bubbles through liquid with sloping plates or elements mounted stepwise
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0053—Details of the reactor
    • B01J19/006—Baffles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00076—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements inside the reactor
    • B01J2219/00085—Plates; Jackets; Cylinders
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00132—Controlling the temperature using electric heating or cooling elements
    • B01J2219/00135—Electric resistance heaters
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00164—Controlling or regulating processes controlling the flow
    • B01J2219/00166—Controlling or regulating processes controlling the flow controlling the residence time inside the reactor vessel
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00168—Controlling or regulating processes controlling the viscosity
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00761—Details of the reactor
    • B01J2219/00763—Baffles
    • B01J2219/00765—Baffles attached to the reactor wall
    • B01J2219/0077—Baffles attached to the reactor wall inclined
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00761—Details of the reactor
    • B01J2219/00763—Baffles
    • B01J2219/00765—Baffles attached to the reactor wall
    • B01J2219/00777—Baffles attached to the reactor wall horizontal

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Other Resins Obtained By Reactions Not Involving Carbon-To-Carbon Unsaturated Bonds (AREA)
  • Polyesters Or Polycarbonates (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Polymerisation Methods In General (AREA)
  • Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
SK1336-96A 1994-05-02 1995-04-21 Split flow reactor trays for vertical staged polycondensation reactors SK133696A3 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US08/238,037 US5466419A (en) 1994-05-02 1994-05-02 Split flow reactor trays for vertical staged polycondensation reactors
PCT/US1995/004892 WO1995029752A1 (en) 1994-05-02 1995-04-21 Split flow reactor trays for vertical staged polycondensation reactors

Publications (1)

Publication Number Publication Date
SK133696A3 true SK133696A3 (en) 1997-09-10

Family

ID=22896238

Family Applications (1)

Application Number Title Priority Date Filing Date
SK1336-96A SK133696A3 (en) 1994-05-02 1995-04-21 Split flow reactor trays for vertical staged polycondensation reactors

Country Status (24)

Country Link
US (1) US5466419A (de)
EP (1) EP0758266B1 (de)
JP (1) JPH09512207A (de)
KR (2) KR970702749A (de)
CN (1) CN1146733A (de)
AT (1) ATE168584T1 (de)
AU (1) AU681791B2 (de)
BR (1) BR9507582A (de)
CA (1) CA2188878C (de)
CO (1) CO4410351A1 (de)
CZ (1) CZ304996A3 (de)
DE (1) DE69503624T2 (de)
ES (1) ES2119437T3 (de)
FI (1) FI964409A7 (de)
HU (1) HUT75812A (de)
IL (1) IL113553A0 (de)
MY (1) MY111462A (de)
NO (1) NO964607D0 (de)
NZ (1) NZ285221A (de)
PL (1) PL317103A1 (de)
SK (1) SK133696A3 (de)
TW (1) TW326405B (de)
WO (1) WO1995029752A1 (de)
ZA (1) ZA953508B (de)

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US6631892B1 (en) * 1998-08-25 2003-10-14 Donald C. Erickson Tray contactor with same direction liquid flow
US6906164B2 (en) 2000-12-07 2005-06-14 Eastman Chemical Company Polyester process using a pipe reactor
CN1900139B (zh) 2000-12-07 2012-11-14 奇派特石化有限公司 制造缩聚物的方法
DE10246251A1 (de) 2002-10-02 2004-04-15 Zimmer Ag Verfahren und Vorrichtung zur kontinuierlichen Herstellung von Polyestern
US7074879B2 (en) 2003-06-06 2006-07-11 Eastman Chemical Company Polyester process using a pipe reactor
US7135541B2 (en) 2003-06-06 2006-11-14 Eastman Chemical Company Polyester process using a pipe reactor
US7332548B2 (en) 2004-03-04 2008-02-19 Eastman Chemical Company Process for production of a polyester product from alkylene oxide and carboxylic acid
DE102004038466B4 (de) * 2004-08-07 2014-08-28 Lurgi Zimmer Gmbh Verfahren und Vorrichtung zur kontinuierlichen Vorpolykondensation von Ver-/Umesterungsprodukten
US7435393B2 (en) * 2005-05-05 2008-10-14 Eastman Chemical Company Baffle assembly module for vertical staged polymerization reactors
US20060251547A1 (en) * 2005-05-05 2006-11-09 Windes Larry C Family of stationary film generators and film support structures for vertical staged polymerization reactors
US7718137B2 (en) * 2005-10-28 2010-05-18 Eastman Chemical Company Reactor with optimized internal tray design
ATE371685T1 (de) * 2006-01-24 2007-09-15 Lurgi Zimmer Gmbh Verfahren zur veresterung von terephthalsäure mit butandiol, verfahren zur herstellung von polybutylenterephthalat und vorrichtung dafür
WO2007122452A1 (en) * 2006-04-21 2007-11-01 Quali Guarantee (Proprietary) Limited Apparatus for producing carbon monoxide by a chemical reaction process
US7649109B2 (en) 2006-12-07 2010-01-19 Eastman Chemical Company Polyester production system employing recirculation of hot alcohol to esterification zone
US7943094B2 (en) 2006-12-07 2011-05-17 Grupo Petrotemex, S.A. De C.V. Polyester production system employing horizontally elongated esterification vessel
US7892498B2 (en) 2007-03-08 2011-02-22 Eastman Chemical Company Polyester production system employing an unagitated esterification reactor
US7863477B2 (en) 2007-03-08 2011-01-04 Eastman Chemical Company Polyester production system employing hot paste to esterification zone
US7868129B2 (en) 2007-07-12 2011-01-11 Eastman Chemical Company Sloped tubular reactor with spaced sequential trays
US7829653B2 (en) * 2007-07-12 2010-11-09 Eastman Chemical Company Horizontal trayed reactor
US7872090B2 (en) 2007-07-12 2011-01-18 Eastman Chemical Company Reactor system with optimized heating and phase separation
US7868130B2 (en) 2007-07-12 2011-01-11 Eastman Chemical Company Multi-level tubular reactor with vertically spaced segments
US7847053B2 (en) 2007-07-12 2010-12-07 Eastman Chemical Company Multi-level tubular reactor with oppositely extending segments
US7872089B2 (en) 2007-07-12 2011-01-18 Eastman Chemical Company Multi-level tubular reactor with internal tray
US7858730B2 (en) 2007-07-12 2010-12-28 Eastman Chemical Company Multi-level tubular reactor with dual headers
US7842777B2 (en) * 2007-07-12 2010-11-30 Eastman Chemical Company Sloped tubular reactor with divided flow
US8197785B2 (en) 2008-02-27 2012-06-12 Kellogg Brown & Root Llc Split flow contactor
DK3013467T3 (en) * 2013-06-28 2018-05-22 Uop Llc FLUID DISTRIBUTION DEVICE AND PROCEDURE FOR MULTI-LEARNING ACTORS
US9669358B2 (en) * 2015-03-10 2017-06-06 Dürr Systems Ag Methods and apparatus for crossflow reactors
JP7073374B2 (ja) * 2016-12-06 2022-05-23 コベストロ、ドイチュラント、アクチエンゲゼルシャフト カスケードトレイ、そのカスケードトレイを備える精留塔、その様な精留塔の運用方法、およびその使用
DE102017106177A1 (de) * 2017-03-22 2018-09-27 Thyssenkrupp Ag Boden für eine Stoffaustauschkolonne

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FR990870A (fr) * 1948-10-29 1951-09-27 Nouvelle Soc Induschimie D Etu Appareil pour le traitement de fluides gazeux
US3017950A (en) * 1960-12-30 1962-01-23 Henry F Koshoot Bubble-plate structure for rectification columns
US3359074A (en) * 1963-06-11 1967-12-19 Monsanto Co Polycondensation apparatus
US3509203A (en) * 1966-12-16 1970-04-28 Engels Chemiefaserwerk Veb Transesterification of dicarboxylic alkyl esters with glycols
US3658484A (en) * 1969-10-24 1972-04-25 Arthur W Bright Countercurrent contact apparatus
DE1957458B2 (de) * 1969-11-15 1973-04-19 Chemische Werke Hüls AG, 4370 Mari Vorrichtung zur kontinuierlichen durchfuehrung chemischer umsetzungen in fluessiger phase
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Also Published As

Publication number Publication date
WO1995029752A1 (en) 1995-11-09
JPH09512207A (ja) 1997-12-09
EP0758266B1 (de) 1998-07-22
TW326405B (en) 1998-02-11
FI964409A0 (fi) 1996-11-01
DE69503624D1 (de) 1998-08-27
MY111462A (en) 2000-05-31
KR970702750A (ko) 1997-06-10
CN1146733A (zh) 1997-04-02
KR970702749A (ko) 1997-06-10
BR9507582A (pt) 1997-09-09
US5466419A (en) 1995-11-14
CA2188878A1 (en) 1995-11-09
HU9603011D0 (en) 1997-01-28
ATE168584T1 (de) 1998-08-15
FI964409A7 (fi) 1996-11-01
AU2425695A (en) 1995-11-29
CO4410351A1 (es) 1997-01-09
ZA953508B (en) 1996-01-15
ES2119437T3 (es) 1998-10-01
NO964607L (no) 1996-10-31
NZ285221A (en) 1997-01-29
AU681791B2 (en) 1997-09-04
PL317103A1 (en) 1997-03-17
NO964607D0 (no) 1996-10-31
DE69503624T2 (de) 1998-11-26
IL113553A0 (en) 1995-08-31
CA2188878C (en) 2000-04-04
EP0758266A1 (de) 1997-02-19
HUT75812A (en) 1997-05-28
CZ304996A3 (en) 1997-09-17

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